Ethanologenic Clostridium species, Clostridium coskatii

ABSTRACT

An isolated clostridia bacterial species ( Clostridium coskatii  ATCC No. PTA-10522, “PS02”) is provided. Under anaerobic conditions  C. coskatii  can convert CO and/or H 2  and/or CO 2  to ethanol or acetate. Thus, this bacterium is capable of transforming waste gases (e.g. syngas and refinery wastes) into useful products.

This application is a divisional application of U.S. patent application Ser. No. 12/727,320 filed Mar. 19, 2010 which is incorporated herein by reference in its entirety.

SEQUENCE LISTING STATEMENT

The sequence listing is filed in this application in electronic format only and is incorporated by reference herein. The sequence listing text file “09-1202 SequenceListing.txt” was created on Apr. 12, 2010, and is 4,863 bytes in size.

FIELD OF THE INVENTION

The field of the invention relates to a novel bacterial species that is capable of producing ethanol from gas mixtures consisting of hydrogen (H₂) and carbon dioxide (CO₂), and/or carbon monoxide (CO). In particular, the invention provides a novel Clostridium species, Clostridium coskatii (PS02), having the identifying characteristics of ATCC No. PTA-10522 and a method of synthesizing ethanol and other useful products from H₂ and/or CO₂, and/or CO gas using this novel Clostridium species.

BACKGROUND OF THE INVENTION

Currently, the major mode of biofuel production (production of fuel, such as ethanol, from biomass) is through direct fermentation, which accounts for 90% of the ethanol output in the U.S. (Licht, F. O. (2001) World Ethanol Markets, Analysis and Outlook, Kent, UK). Direct fermentation is the process in which a saccharolytic microorganism, such as yeast or bacteria, converts sugars to ethanol. These sugars may be simple (i.e. glucose) or complex (i.e. starch, cellulose, hemicellulose). Corn starch is the primary substrate used in ethanol producing plants today. One disadvantage of the use of corn starch in the direct fermentation production of ethanol is that corn is a component of many human and animal foods. Therefore, the use of the corn for the production of ethanol takes it out of the supply for human and animal consumption.

Other substrates, such as lignocellulosic biomass (i.e. grasses, small trees, paper waste, or saw dust), are also being researched for use in direct fermentation of biofuels. However, they also have limitations. Lignocellulose is comprised of cellulose, hemicellulose, pectin, and lignin, which require pretreatment processes to break down the biomass into its individual sugar components before microorganisms can utilize the substrate. This adds more cost in the areas of materials, plant design, and waste management. Furthermore, approximately 22-35% of the lignocellulose fraction is composed of lignin, which cannot be utilized by current direct fermentation approaches, and is discarded from the process as a recalcitrant waste material.

Another alternative method of biofuel production is indirect fermentation. Indirect fermentation is the process in which energy-rich gases which can provide an electron source, such as H₂ and CO, and carbon sources, such as CO and CO₂ are generated from carbon-containing, non-food agricultural and industrial waste material, and then are transferred to a bioreactor where anaerobic bacteria convert the gases to biofuels. The gases produced when lignocellulosic biomass is pyrolyzed (burned) would be an example of a type of waste gas that may be utilized in indirect fermentation. Synthesis gas (also referred to as “syngas”) (primarily CO, H₂, and CO₂) is a product of pyrolyzed biomass or coal and has been recognized for its potential role in the indirect fermentation of biomass to fuel alcohol (Zeikus, J. G, Annu Rev. Microbiol. 34:423-464 (1980)). Another source of energy-rich waste gas is the basic oxygen steelmaking (LD converter) process, which produces a significant volume of waste gas consisting of 70% CO, 1-2% H₂, and 10-15% CO₂, which is also suitable for producing biofuels using the indirect fermentation process.

Anaerobic microorganisms such as acetogenic bacteria offer a viable route to convert waste gases to useful products, such as ethanol and n-butanol, via the indirect fermentation process. Such bacteria catalyze the conversion of H₂ and CO₂ and/or CO to biofuels with higher specificity, higher yields and lower energy costs than can be attained by the Fischer-Tropsch process, or other chemical biofuel production processes that use CO and H₂. Several microorganisms capable of producing biofuels from waste gases and other substrates have been identified and are discussed below.

Six acetogenic bacteria have been described for use in the production of the biofuels, ethanol, n-butanol, or mixtures of these alcohols using at least one of the three main components of syngas (H₂+CO₂, or CO, or H₂+CO₂ and CO) as substrates. These include Butyribacterium methylotrophicum (Grethlein et al., 1990; Jain et al., 1994b), Clostridium ragsdalei (Huhnke et al., 2008), Clostridium carboxidivorans (Liou, et al., 2005), Moorella species HUC22-1 (Inokuma, et al., 2007), Clostridium autoethanogenum (Abrini et al., 1994), and Clostridium ljungdahlii (Arora et al, 1995; Batik et al., 1988; Batik et al. 1990; and Tanner et al., 1993). Of these representatives, only three—Clostridium ljungdahlii, Clostridium ragsdalei, and Clostridium autoethanogenum—are known to convert CO, or mixtures of CO and/or H₂ and CO₂ to acetic acid and ethanol. Thus, they are the only known organisms capable of forming a single alcohol (ethanol) end product, while simultaneously using all components of a synthesis gas stream. This group of bacteria, referred to in this document as the clostridial ethanologens, have significant commercial importance because the economics of the indirect fermentation process is advantaged by: (a) co-utilization of H₂ and CO, so that the combined conversion rate exceeds 90%, and (b) production of a single alcohol, which permits the use of a simplified and less expensive biofuel recovery system.

Six clostridial ethanologens have been described in literature for the production of biofuels from synthesis gas:

(1) Clostridium ljungdahlii PETC^(T) (ATCC No. 49587 and DSMZ No. 13528): This organism is the original type strain deposit for this species (Tanner et al., 1993). See U.S. Pat. No. 5,173,429.

(2) Clostridium ljungdahlii ERI-2 (ATCC No. 55380): The phylogenetic status of this organism remains unclear since it is apparently not identical to the PETC type strain, but is not included on the list of Approved Lists of Bacterial Names (Skerman et al., 1989). See U.S. Pat. No. 5,593,886. (3) Clostridium ljungdahlii C-01; (ATCC No. 55988): The phylogenetic status of this organism remains unclear since it is apparently not identical to the PETC type strain, but is not included on the list of Approved Lists of Bacterial Names (Skerman et al., 1989). See U.S. Pat. No. 6,136,577. (4) Clostridium ljungdahlii O-52; (ATCC No. 55989): The phylogenetic status of this organism remains unclear since it is apparently not identical to the PETC type strain, but is not included on the list of Approved Lists of Bacterial Names (Skerman et al., 1989). See U.S. Pat. No. 6,136,577. (5) Clostridium ragsdalei; (ATCC No. BAA-622): See U.S. Pat. No. US20080057554 (EP2061872A2). (6) Clostridium autoethanogenum; (DSMZ No. 10061) This isolate was described by Abrini et al., 1994 as producing ethanol and acetate from mixtures of CO, H₂, and CO₂.

In addition to patents describing the use of specific ethanologenic clostridia for biofuel production, as defined above, the following process patents exist for producing biofuels from waste gases such as synthesis gas. Certain patents also cover microorganisms known to produce multiple alcohols (primarily ethanol and n-butanol) from waste gases (e.g., Clostridium carboxidivorans):

(1) U.S. Pat. No. US20070275447A1 to Lewis et al. discloses Clostridium carboxidivorans ATCC No. BAA-624, a novel anaerobic clostridia bacterial species that is capable of synthesizing biofuels, including ethanol and n-butanol from waste gases such as synthesis gas. (2) U.S. Pat. No. 5,192,673 to Jain et al. discloses a mutant strain of Clostridium acetobytylicum and a process for making butanol with the strain. (3) U.S. Pat. No. 5,593,886 to Gaddy et al. discloses a process using Clostridium ljungdahlii ATCC No. 55380 for producing acetate and ethanol using waste gas (e.g. carbon black waste gas) as a substrate. (4) U.S. Pat. No. 5,807,722 to Gaddy et al. discloses a method and apparatus for converting waste gases into useful products such as organic acids and alcohols using anaerobic bacteria, such as Clostridium ljungdahlii ATCC No. 55380. (5) U.S. Pat. No. 6,136,577 to Gaddy et al. discloses a method and apparatus for converting waste gases into useful products such as organic acids and alcohols (particularly ethanol) using anaerobic bacteria, such as Clostridium ljungdahlii ATCC Nos. 55988 and 55989. (6) U.S. Pat. No. 6,136,577 to Gaddy et al. discloses a method and apparatus for converting waste gases into useful products such as organic acids and alcohols (particularly acetic acid) using anaerobic strains of Clostridium ljungdahlii. (7) U.S. Pat. No. 6,753,170 to Gaddy et al. discloses an anaerobic microbial fermentation process for the production of acetic acid. (8) U.S. Pat. No. 7,285,402 to Gaddy et al. discloses an anaerobic microbial fermentation process for the production of ethanol.

Despite the knowledge in the art regarding the use of microorganisms in the production of biofuels, there remains an ongoing need to discover and/or develop additional microorganisms that are capable of producing useful products such as biofuels using the indirect fermentation process. In particular, it would be advantageous to discover new ethanologenic clostridia that exhibit improved growth characteristics and high biofuel yields when cultivated under chemically-defined or low organic carbon growth conditions. Specifically, elimination of complex organic carbon sources such as yeast extract, beef extract, corn steep liquor, or soy tryptones from the bacterial growth medium could be considered desirable for production of biofuels via synthesis gas fermentation because (1) these components add additional expense to the biofuels production cost, and (2) complex organic carbon sources support foreign bacterial growth in the biofuels production fermentors, which negatively impacts biofuel yield and process economics.

SUMMARY OF INVENTION

The present invention is directed to a biologically pure culture of a newly discovered ethanologenic Clostridia species, Clostridium coskatii (PS02). This Clostridia species is a new Clostridia species with distinguishing phenotypic and genetic characteristics from other known Clostridia species.

Another embodiment of the present invention is the unique capability of this Clostridia species to produce ethanol and acetate from gaseous sources of CO and/or H₂ and/or CO₂.

In another embodiment of the present invention, the Clostridium coskatii is uniquely capable of ethanol production in the absence of complex organic carbon sources, such as yeast extract.

BRIEF DESCRIPTION OF DRAWINGS

FIG. 1 is a transmission electron micrograph of a negative stained [phase, 25,000× magnification. Bar=1.0 μm.

FIG. 2 is a phase-contrast light micrograph of Clostridium coskatii (PS02) cells during stationary phase, 1,000× magnification. Bar=14.63 μm.

FIG. 3 is a scanning electron micrograph of Clostridium coskatii (PS02) cells harvested during late log phase growth, 10,000× magnification. Bar=1.0 μm.

FIG. 4 illustrates the pH growth optimum based on optical density for a batch culture of Clostridium coskatii (PS02) compared to Clostridium autoethanogenum.

FIG. 5 illustrates the pH growth optimum for a batch culture of Clostridium coskatii (PS02) based on volumetric concentration of the end products, ethanol and acetate.

FIG. 6 illustrates the temperature growth optimum of Clostridium coskatii (PS02) based on optical density.

FIG. 7 a illustrates a comparison of fatty acid methyl ester profiles for ethanologenic clostridia: (A) C. ljungdahlii PETC; (B) C. autoethanogenum; (C) C. ragsdalei; (D) C. coskatii (PS02). Compounds and corresponding peaks: (1) Methyl dodecanoate (8.161 minutes); (2) tetradecanal (10.046 minutes); (3) methyl tetradecanoate (12.61 minutes); (4) 1,1-dimethoxy-dodecane (13.881 minutes); (5) 1-methyl dodecylamine (15.176 minutes); (6) (Z)-13-octadecenal, (17.638 minutes); (7) methyl hexadecanoic acid, (18.138 minutes); (8) methyl-6,6-dimethoxy-octanoic acid (18.973 minutes); (9) 1,1-dimethoxy-tetradecane, (19.506 minutes); (10) cyclopropaneoctanoic acid, 2-hexyl-, methyl ester (20.735 minutes); (11) 1,1-dimethoxy-hexadecane (22.113 minutes); (12) 2-Oxo-3-methyl-cis-per hydro-, 1,3-benzoxazine (23.363 minutes).

FIG. 7 b provides a matrix of correlation coefficients summarizing the strength of the linear relationships in fatty acid methyl ester profiles of FIG. 7 a.

FIG. 7 c illustrates a scatterplot matrix showing the strength of the linear relationships in fatty acid methyl ester profiles of FIG. 7 b; α=0.99.

FIG. 8 a illustrates SEQ ID NO. 3, which is the 16S rDNA sequence for Clostridium coskatii. Gaps in the contiguous sequence were generated by alignment to sequences shown in FIG. 8 b.

FIG. 8 b illustrates a 16S rDNA parsimony tree of clostridial species. Bar corresponds to 1 nucleotide substitution per 100 sequence positions. The distance of the ethanologenic clostridial cluster (C. coskatii PS02) to other selected clostridium cluster I representatives is: C. tyrobutyricum: 95.18%; C. magnum: 93.01%; C. kluyveri: 92.96%; C. scatologenes: 92.52%.

FIG. 9 illustrates a 16S rDNA neighbor phylogenetic tree distance matrix scores showing similarity of the 16S rDNA sequence for ethanologenic clostridia.

FIG. 10 illustrates an entrophy plot showing the frequency of hypervariable regions in the 16S rDNA sequences for the six ethanologenic acetogens and the sequence alignment of those hypervariable regions.

FIG. 11 illustrates a BOX-PCR comparison of ethanologenic clostridial species. Lane assignments are: (1) 100 bp ladder; (2) C. coskatii (PS02); (3) C. ragsdalei ATCC BAA-622; (4) C. autoethanogenum DSMZ 10061; (5) C. ljungdahlii PETC DSMZ 13528; (6) C. ljungdahlii C-01 ATCC 55988; (7) C. ljungdahlii ERI-2 ATCC 55380; (8) 100 bp ladder; (9) pUC19/Sau3A marker.

FIG. 12 illustrates a Parsimony tree and Pearson UPGMA similarity matrix scores for the analysis of amplicons generated by BOX-PCR for ethanologenic clostridial species.

FIG. 13 illustrates a REP-PCR comparison of ethanologenic clostridial species. Lane assignments are: (1) 100 bp ladder; (2) C. coskatii (PS02); (3) C. ragsdalei ATCC BAA-622; (4) C. autoethanogenum DSMZ 10061; (5) C. ljungdahlii PETC DSMZ 13528; (6) C. ljungdahlii C-01 ATCC 55988; (7) C. ljungdahlii ERI-2 ATCC 55380; (8) 100 bp ladder; (9) pUC19/Sau3A marker.

FIG. 14 illustrates a Parsimony tree and Pearson UPGMA similarity matrix scores for the analysis of amplicons generated by REP-PCR for ethanologenic clostridial species.

FIG. 15 illustrates an ERIC-PCR comparison of ethanologenic clostridial species. Lane assignments are: (1) 100 bp ladder; (2) C. coskatii (PS02); (3) C. ragsdalei ATCC BAA-622; (4) C. autoethanogenum DSMZ 10061; (5) C. ljungdahlii PETC DSMZ 13528; (6) C. ljungdahlii C-01 ATCC 55988; (7) C. ljungdahlii ERI-2 ATCC 55380; (8) 100 bp ladder; (9) pUC19/Sau3A marker.

FIG. 16 illustrates a Parsimony tree and Pearson UPGMA similarity matrix scores for the analysis of amplicons generated by ERIC-PCR for ethanologenic clostridial species.

FIG. 17 illustrates specific growth rate measurements of Clostridium coskatii (PS02) when using Acetogen C5 media and in a synthesis gas-fed CSTR: (a) under pre-steady state conditions (exponential growth phase), and (b) under ethanol production phase (late exponential to stationary phase) using a mean cell retention time of 2.0 days. Duration=43.75 days.

FIG. 18 is an X-ray spectrum showing the major elements present in Clostridium coskatii (PS02) cells.

FIG. 19 illustrates the volumetric concentration of ethanol and acetate produced in a synthesis gas-fed CSTR using Acetogen C5 media, using a 2.0 day mean cell retention time, and containing Clostridium coskatii (PS02). Duration=43.75 days.

FIG. 20 illustrates the gas uptake rate for a synthesis gas-fed CSTR (products shown in FIG. 21) when using Ethanologen C5 media, a 2.0 day mean cell retention time, and containing Clostridium coskatii (PS02). Duration=43.75 days.

FIG. 21 illustrates the GC-MS total ion current (TIC) chromatogram of volatiles present in the broth phase of a syngas fermentation at a steady-state growth for Clostridium coskatii (PS02). Inset: 28-fold magnification of the chromatographic baseline showing trace impurities generated through metabolism (formic acid, ethyl ester) or acid-catalyzed chemical reaction (ethyl acetate).

FIG. 22 a: Statistical analysis for the average gas uptake rate for a 470 hour steady-state period in a synthesis gas-fed CSTR using Acetogen C5 media, a 2.0 day mean cell retention time, and containing Clostridium coskatii (PS02). Duration=43.75 days. A) CO uptake, B) H₂ uptake, and C) CO₂ uptake.

FIG. 22 b illustrates a continuation of the statistical analysis for the average gas uptake rate for a 470 hour steady-state period in a synthesis gas-fed CSTR using Acetogen C5 media, a 2.0 day mean cell retention time, and containing Clostridium coskatii (PS02). Duration=43.75 days. A) Volumetric ethanol concentration in mmol/L, B) Volumetric ethanol concentration in mmol/L, and C) total ethanol vented from the broth in mmol/L.

FIG. 23 illustrates the effect of organic carbon (yeast extract) addition on ethanol and acetate production by a synthesis gas-fed CSTR containing Clostridium coskatii. (A) Ethanol production in 2 L CSTR (D=0.5 day⁻¹) receiving a chemically-defined minimal media (Acetogen C5), or the same media supplemented with 0.1 g/L yeast extract. (B) Acetate production in 2 L CSTR (D=0.5 day⁻¹) receiving a chemically-defined minimal media, or the same media supplemented with 0.1 g/L yeast extract

DETAILED DESCRIPTION OF EMBODIMENTS

The bacterium of the present invention is a novel ethanologenic Clostridia species which displays the characteristics represented by ATCC No. PTA-10522, herein referred to as “Clostridium coskatii (PS02)”. The phylogenetic, morphological, and biochemical properties of Clostridium coskatii (PS02) have been analyzed and are described in the Examples section below. While certain properties of Clostridium coskatii (PS02) are similar to other Clostridial species, Clostridium coskatii (PS02) possesses unique characteristics that confirm it is a novel species of this genus. The data included in the examples shows that this bacterium is a new representative of the Clostridium genus.

Clostridium coskatii (PS02) has the ability, under anaerobic conditions, to produce acetic acid and ethanol from the substrates, CO+H₂O, or H₂+CO₂, or CO+H₂+CO₂. The CO or CO₂ provide the carbon source and the H₂ or CO provide the electron source for the reactions producing acetic acid and ethanol. The primary product produced by the fermentation of CO and/or H₂ and CO₂ by Clostridium coskatii (PS02) is ethanol, according to the following reactions: 6CO+3H₂O→C₂H₅OH+4CO₂  (1) 6H₂+2CO₂→C₂H₅OH+3H₂O  (2)

Clostridium coskatii (PS02) may also produce acetate. Acetate production occurs via the following reactions: 4CO+2H₂O→CH₃COOH+2CO₂  (3) 4H₂+2CO₂→CH₃COOH+2H₂O  (4)

Many sources of CO, CO₂ and H₂ may be utilized by the Clostridium of the present invention. For example, preferred sources of these substrates include “waste” gases such as syngas, oil refinery waste gases, steel manufacturing waste gases, autothermal reforming of natural gas, and coal gasification. Sources also include gases (containing some H₂) which are produced by yeast, clostridial fermentations, and gasified cellulosic materials. Alternatively, such gaseous substrates are not necessarily produced as byproducts of other processes, but may be produced specifically for use in the fermentation reactions of the invention, which utilize Clostridium coskatii (PS02). Those of skill in the art will recognize that any source of substrate gas may be used in the practice of the present invention, so long as it is possible to provide the Clostridium coskatii with sufficient quantities of the substrate gases under conditions suitable for the bacterium to carry out the fermentation reactions.

In one preferred embodiment of the invention, the source of CO, CO₂ and H₂ is syngas. Syngas for use as a substrate may be obtained, for example, as a gaseous byproduct of coal gasification. Alternatively, syngas can be produced by gasification of readily available low-cost agricultural raw materials expressly for the purpose of bacterial fermentation, thereby providing a route for indirect fermentation of biomass to fuel alcohol. There are numerous examples of raw materials which can be converted to syngas, as most types of vegetation could be used for this purpose. Preferred raw materials include but are not limited to perennial grasses such as switchgrass, crop residues such as corn stover, processing wastes such as sawdust, etc. Those of skill in the art are familiar with the generation of syngas from such starting materials. In general, syngas is generated in a gasifier from dried biomass primarily by pyrolysis, partial oxidation, and steam reforming, the primary products being CO, H₂ and CO₂. The terms “gasification” and “pyrolysis” refer to similar processes; both processes limit the amount of oxygen to which the biomass is exposed. The term “gasification” is sometimes used to include both gasification and pyrolysis.

Combinations of sources for substrate gases fed into the indirect fermentation process may also be utilized to alter the concentration of components in the vent stream from the bioreactor. For example, the primary source of CO, CO₂ and H₂ may be syngas, which typically exhibits a concentration ratio of 37% CO, 35% H₂, and 18% CO₂, but the syngas may be supplemented with gas from other sources to enrich the level of CO (i.e., steel mill waste gas is enriched in CO) or H₂.

The Clostridium coskatii of the present invention must be cultured under anaerobic conditions. “Anaerobic conditions” means the level of oxygen (O₂) is below 0.5 parts per million in the gas phase.

The source of H₂O for the reaction represented by Equations (1) or (3) is typically the aqueous media in which the organism is cultured.

In general, the optimized ethanol production media for culturing the acetogen of this invention is a liquid medium that is chemically-defined. However, those of skill in the art will recognize that alternative media can be utilized, for example, ATCC medium 1045 under a H₂:CO₂ or CO:CO₂ atmosphere at an initial pH of 6. Further, various media supplements may be added for any of several purposes, e.g. buffering agents, metals, vitamins, and salts. In particular, those of skill in the art are familiar with such techniques as nutrient manipulation and physiological adaptation, which result in increased or optimized yields of a bioproduct. For example, culturing solvent-producing microbes under “limited-growth” conditions (i.e. conditions which slow the rate of bacterial growth and reproduction) result in enhanced production of highly reduced fermentation products such as ethanol. This is likely because under limited-growth conditions, the ratio of available reducing equivalents (reduced ferridoxin, NADH, or NADPH) to available carbon increases, and the increased reducing power is diverted into chemical reduction of acetyl Co-A or organic acids to form alcohols. Examples of limited-growth conditions include, for example, maintaining the culture at non-optimal temperature or pH, and the limitation of nutrients and carbon sources. Generally, non-growth conditions would be implemented after a desired density of bacteria is reached in the culture. Those of skill in the art are familiar with procedures for optimizing the production of desired products, and all such optimized procedures using Clostridium coskatii (PS02) are intended to be encompassed by the present invention.

In particular, Clostridium coskatii (PS02) may be cultured using the Balch technique (Balch and Wolfe, 1976, Appl. Environ. Microbiol. 32:781-791; Balch et al., 1979, Microbiol. Rev. 43:260-296). This entails the aid of an anaerobic chamber for preparing culture materials and a gas exchange manifold to establish whatever gas phase is desired for culture in sealed tubes or vessels. More specific details on culturing solvent-producing acetogens, such as the use of an acidic pH, appear in Tanner et al., 1993, Int. J. Syst. Bacteriol. 43:232-236 and Liou et al., 2005, Int. J. Syst. Evol. Microbiol. 55:2085-2091. Methods to enhance ethanol production include optimization of key medium components (such as iron, phosphate and vitamins), control of culture pH, random mutagenesis of the bacterium followed by clonal screening, or genetic engineering of the bacterium.

The metabolism of gases (CO and/or H₂ and CO₂) supplied to the fermentation by Clostridium coskatii (PS02) can be carried out in any of several types of apparatuses that are known to those of skill in the art, with or without additional modifications, or in other styles of fermentation equipment that are currently under development. Examples include but are not limited to bubble column reactors, two stage bioreactors, trickle bed reactors, membrane reactors, packed bed reactors containing immobilized cells, etc. The chief requirements of such an apparatus include:

-   -   (1) Axenicity;     -   (2) Anaerobic conditions;     -   (3) Suitable conditions for maintenance of temperature,         pressure, and pH;     -   (4) Sufficient quantities of substrates are supplied to the         culture;     -   (5) The end products of the fermentation can be readily         recovered from the bacterial broth.

The reactor may be, for example, a traditional stirred tank reactor, a column fermentor with immobilized or suspended cells, a continuous flow type reactor, a high pressure reactor, a suspended cell reactor with cell recycle, and other examples previously listed. Furthermore, reactors may be arranged in a series and/or parallel reactor system which contains any of the above-mentioned reactors. For example, multiple reactors can be useful for growing cells under one set of conditions and generating ethanol (or other products) with minimal growth under another set of conditions.

In general, fermentation will be allowed to proceed until a desired level of product such as ethanol is produced in the culture media. Typically, this level of ethanol is in the range of at least 15 grams/liter of culture medium to 50 grams/liter, with a level of at least 30 grams/liter being preferable. Clostridium coskatii (PS02) remains viable and will grow in ethanol concentrations of at least 60 grams/liter. Alternatively, production may be halted when a certain rate of production is achieved, e.g. when the rate of production of a desired product has declined due to, for example, build-up of bacterial waste products, reduction in substrate availability, feedback inhibition by products, reduction in the number of viable bacteria, or for any of several other reasons known to those of skill in the art. In addition, continuous culture techniques exist which allow the continual replenishment of fresh culture medium with concurrent removal of used medium, including any liquid products therein (i.e. the chemostat mode).

The products that are produced by the bacterium of this invention can be removed from the culture and purified by any of several methods that are known to those of skill in the art. For example, ethanol can be removed and further processed, e.g. by solvent extraction; distillation to the azeotrope followed by azeotropic distillation; molecular sieve dehydration; pervaporation; or flow-through zeolite tubes. Those of skill in the art will recognize that the two main techniques in industry for ethanol dehydration following distillation are azeotropic distillation and molecular sieve dehydration. In addition, depending on the number of products, several separation techniques may need to be employed to obtain several pure products. Likewise, acetate may be removed and further processed by similar processes.

Clostridium coskatii (PS02) was obtained from an anaerobic enrichment inoculated with estuary sediment collected from Coskata-Coatue Wildlife Refuge in Nantucket, Mass. by a procedure described previously (Bryant, 1972) in 125 mL serum vials under an atmosphere of CO:H₂:N₂:CO₂ (7:37:33:23 mole %) and an initial pH of 6.0, using Acetogen C3 medium, such as described below. A master cell bank was prepared from biomass acquired from single colony isolates picked from agar-containing (15% w:v) petri plates, using the Acetogen C3 medium and an atmosphere of H₂ (5%), CO₂ (10%), and N₂ (85%). This bacterium was deposited with the American Type Culture Collection as strain ATCC No. PTA-10522 on Dec. 10, 2009 under the terms of the Budapest Treaty.

Several phylogenetically diverse groups of anaerobic bacteria have the ability to convert CO, CO₂ and H₂ to a variety of commercially-important products including acetate, ethanol, butyrate, butanol, and hydrogen. A select subgroup, the ethanologenic Clostridia, exhibit the unique ability to simultaneously utilize hydrogen and carbon monoxide to form ethanol, along with small amounts of acetate while using carbon dioxide as a carbon source. The phylogenetic, morphological, and biochemical properties of Clostridium coskatii (PS02) have been analyzed and compared against other similar Clostridial species.

Other Clostridial species utilized in these comparison studies included: Clostridium ljundahlii PETC (ATCC No. 49587 or DSMZ No. 13528); C. ragsdalei (ATCC BAA-622); C. autoethanogenum (DSMZ No. 10061); C. ljundgahlii ERI-2 (ATCC No. 55380); and C. ljungdahlii C-01 (ATCC No. 55988). ATCC samples were obtained from the American Type Culture Collection (ATCC; Manassas, Va.). DSMZ samples were obtained from Deutsche Sammlung von Mikroorganismen and Zellkulturen (DSMZ) GmbH (Braunschweig, Germany). However, as of Feb. 1, 2010, Clostridium ljungdahlii O-52 is no longer publically available because the depositor has terminated supply activities with the American Type Culture Collection.

EXAMPLE 1 Cellular Morphology

Colonies of Clostridium coskatii (PS02) appeared circular, were white to translucent in color, and slightly raised at the center on Acetogen C3 agar plates. The color darkened to tan or light brown when the colony age exceed 6-7 days. Cells of Clostridium coskatii (PS02) were rarely motile, rod-shaped, stained gram-positive, and occurred singly or in chains. An outer cellular structure consistent with a 40 to 45 nm cell wall was seen in electron micrographs of thin sections of C. coskatii cells, which supports the gram-positive assignment. In early exponential growth, cells were 0.75 μm by 3-4 μm and were peritrichously flagellated (FIG. 1). Spores occurred infrequently, but when present appeared as mid-terminal to terminal swelling, and were most often club-like in appearance (FIG. 2). This property of spore morphology was similar to Moorella thermoacetica (Drake et al., 2006), but significantly different than the non-swelling spore morphology observed for Clostridium autoethanogenum (Abrini et al., 1994) or Clostridium ragsdalei (Huhnke et al., 2008). Comparison of electron micrographs for cells in early and late exponential growth showed that cells increased in their length during later phases of growth (FIG. 3). Elongation of the cells up to 20-30 μm was observed for aged batch cultures exhibiting high volumetric ethanol concentrations, and appeared to be related to physiological stress, since these cells were not easily recovered when transferred to a fresh medium. Sporulation was not observed in elongated cells, which likely contributed to the inability to recover these cells.

Acetogen C3 medium was used to initiate preserved cultures taken from a lyophilized or frozen master cell bank (1 mL equivalent volume). Cultures used in this example were grown at a temperature of 37° C. on an orbital shaker at 100 rpm (5 cm shaking amplitude). The culture medium was prepared using the strict anaerobic technique described by Balch and Wolfe (1976), as detailed in Tables A, B, D, and E below. After sterilization, an anaerobic vitamin solution (Table C) was aseptically added to the bottles, and the headspace of each bottle was exchanged with a gas mixture consisting of CO:H₂:N₂:CO₂ (7:37:33:23 mole %), using a final pressure of 104 kPa (15 psig). Standard inoculum size was 10% (v/v), which was transferred from a stock culture that was growing in mid to late exponential phase.

The pH of batch fermentations was controlled using 2-(N-morpholino)ethanesulfonic acid (MES; pK_(a)=5.97 at 37° C.) at a concentration of 20 g/L (pH 6.0). As a replacement to MES, the following buffers were used at a concentration of 20 g/L to conduct pH growth optimum studies: MES (pH 4-6.5), piperazine-N,N′-bis(2-ethanesulfonic acid (PIPES; pH 6.6 to 7.5; pK_(a)=6.66 at 37° C.), and Tris(hydroxymethyl)aminomethane (TRIS; pH 7.5 to 8.5; pK_(a)=7.72 at 37° C.).

TABLE A Mineral stock solution Item Component Amount, g/L 1 NaCl 80 2 NH₄Cl 100 3 KCl 10 4 KH₂PO₄ 10 5 MgSO₄•7H₂O 20 6 CaCl₂•2H₂O 4

TABLE B Trace metals stock solution. Item Component Amount, g/L 1 Hydrochloric acid, 12.1N 2.360 2 MnSO₄•H₂O 1.0 3 FeSO₄•7H₂O 2.2 4 CoCl₂•6H₂O 0.2 5 ZnSO₄•7H₂O 1.0 6 NiCl₂•6H₂O 0.2 7 Na₂MoO₄•2H₂O 0.02 8 Na₂SeO₄ 0.1 9 Na₂WO₄ 0.2

TABLE C Vitamin stock solution. Item Component Amount, mg/L 1 Pyridoxine, HCl 10 2 Thiamine, HCl 5 3 Calcium pantothenate 5 4 Nicotinic acid 5 5 Biotin 2

TABLE D Reducing agent stock solution. Item Component Amount, g/L 1 Cysteine (free base) 40 2 Na₂S•2H₂O 40

TABLE E Final formulation of Acetogen C3 medium. Item Component Amount 1 Minerals stock solution 25 mL/L 2 Trace metals solution 10 mL/L 3 Vitamin stock solution 20 mL/L 4 Yeast extract 0.5 g/L 5 2-(N-morpholino)ethanesulfonic acid 20 g/L 6 5N KOH Adjust pH to 6.0 7 Reducing agent 2.5 mL/L 8 0.1% aqueous resazurin 1 mL/L

Exponential-phase cells grown on Acetogen C3 medium or late-exponential-phase cells growth in CSTRs on Acetogen C5 medium were used for scanning and transmission electron microscopy. Acetogen C5 medium was essentially the same as Acetogen C3 medium, except that sodium sulfide, yeast extract, and the MES buffer were omitted, and an antifoam, such as Antifoam A (Sigma Chemical, St. Louis, Mo.) was added to the medium at a final concentration of 20 mg/L. The samples were examined using a Hitachi S-570 scanning electron microscope, equipped with a Delta 4 Quantum thin-window X-ray detector for simultaneous image and elemental analysis of bacterial cells. For transmission electron microscopy, cells (approximately 1×10²⁰) were fixed in solution with 4% glutaraldehyde in PBS, spread onto carbon coated Formvar grids, and stained with 0.5% phosphotunsgate (pH 7.0). Cells were examined and photographed using a JEOL 1200 EX FX transmission electron microscope. Light microscopy was performed wet mount preparations of fermentation broth using a Nikon Eclipse 50i photomicroscope equipped with Nikon NIS-Elements image acquisition software (Nikon Instruments, Melville, N.Y.).

EXAMPLE 2 Physiology

Clostridium coskatii (PS02) was strictly anaerobic. Chemolithoautotrophic growth in the absence of yeast extract, occurred with H₂+CO₂ or CO. Chemoorganotrophic growth was observed with the following substrates: Pyruvate, succinate, citrate, malate, xylose, mannose, fructose, glucose, salacin, arginine, glutamate, histidie, glutamine, serine, alanine, alpha-ketoglutarate, oxaloacetate, phosphoenol pyruvate, shikimic acid, iso-citrate, sucrose, and malonic acid. Table F shows a substrate matrix comparison between Clostridium coskatii (PS02).

Six organic substrates differentiated C. coskatii from three ethanologenic Clostridia: C. ljungdahlii PETC, C. ragsgalei, and C. ljungdahlii. These differentiating substrates included D-gluconic acid, citrate, maleic acid, rhamnose, arginine, and oxaloacetic acid (Table F). These differences indicate differences in the metabolic regulation or catabolic genes required for metabolism of these substrates among these four bacteria.

-   -   (1) Clostridium coskatii (PS02) and C. autoethanogenum could be         distinguished by the inability of C. coskatii to grow on         D-gluconic acid and rhamnose, and also the inability of C.         autoethanogenum to grow on citrate.     -   (2) Clostridium coskatii (PS02) and C. ragsdalei could be         distinguished by the inability of C. ragsdalei to grow on         citrate, maleic acid, histidine, oxaloacetic acid, and arginine.     -   (3) Clostridium coskatii (PS02) and C. ljungdahlii PETC could be         distinguished by the inability of C. coskatii to grow on         D-gluconic acid, and rhamnose, and also the inability of C.         ljungdahlii PETC to grow on citrate.

TABLE F Growth on various substrates of Clostridial species C. C. C. C. ljungdahlii coskatii Substrate autoethangenum ragsdalei PETC PS02 CO + + + + H₂ + CO₂ + + + + D-Gluconic + − + − Acid Na-Formate − − − − Na-Acetate − − − − Na-Lactate − − − − Na-Pyruvate + + + + Na-Propianate − − − − Na-Succinate + + + + Na-Citrate − − − + Malic acid + + + + Na-Fumerate − − − − Maleic acid + − + + Lactose − − − − Arabinose − − − − Xylose + + + + Mannose + + + + Fructose + + + + Glucose + + + + Methanol − − − − Ethanol + + + + Iso-Propanol − − − − 1-Propanol − − − − Butanol − − − − Rhamnose + − + − Sorbitol − − − − Cellibiose − − − − Salicin + + + + Starch − − − − Arginine + − + + Glutamate + + + + Histidine + − + + Glutamine + + + + Serine + + + + Alanine + + + + D-Ribose − − − − Alpha- + + + + ketoglutarate Oxaloacetic + − − + acid Phosphoenol- + + + + pyruvate Shikimic acid + + + + Glycerol − − − − Iso-Citrate + + + + Sucrose + + + + Galactose − − − − Malonic acid + + + + D-Maltose − − − −

Growth was measured spectrophotometrically at 600 nm (Spectronic 20D; Milton Roy). Carbon substrate utilization was based upon growth after consecutive transfers in media containing 1 g/L of each carbon source. For carbon substrates, screening was performed under an atmosphere of N₂: CO₂ (80%:20%). A positive growth response was recorded for an OD600 exceeding 0.2 AU. For citrate, additional ¹³C-labeled isotope experiments were conducted to determine the nature of products by analysis of final 0.2 μm-filtered product samples by carbon NMR using a Bruker UltraShield Avance 400 MHz nuclear magnetic resonance spectrometer.

EXAMPLE 3 Antibiotic Susceptibility

The antibiotic susceptibility of Clostridium coskatii (PS02) was evaluated in Acetogen C3 media against 17 antibiotics at a concentration of 100 μg/mL (Table G). Clostridium coskatii (PS02) was resistant to erythromycin, nalidixic acid, spectinomycin, colistin, penicillin, streptomycin, and chloramphenicol. Three antibiotics differentiated C. coskatii from three ethanologenic Clostridia: C. ljungdahlii PETC, C. ragsgalei, and C. autoethanogenum. These differentiating antibiotics included, erythromycin, carbenicillin, and chloramphenicol (Table J). Resistance to erythromycin and carbenicillin was shared by Clostridium coskatii (PS02) and Clostridium ljungdahlii PETC; however, resistance to chloramphenicol was trait demonstrated only by Clostridium coskatii (PS02).

TABLE G Antibiotic susceptibility patterns for various clostridial species using an antibiotic concentration of 100 μg/ml (+ indicates growth). C. C. C. C. ljungdahlii coskatii Antibiotic autoethangenum ragsdalei PETC PS02 Ampicillin − − − − Erythromycin − − + + Nalidixic acid + + + + Spectinomycin + + + + Vancomycin − − − − Colistin + + + + Carbenicillin − − + + Gentamicin − − − − Penicillin + + + + Streptomycin + + + + Chloramphenicol − − − + Kanamycin − − − − Paromomycin − − − − Tetracylcine − − − − Lincomycin − − − − Rifampicin − − − − Tylosin − − − −

Antibiotic susceptibility was based upon growth in media containing 100 μg/mL of each antibiotic. The atmosphere was 37% CO, 35% H₂, 22% CO₂ with a balance gas of N₂. A positive growth response was recorded for an OD600 exceeding 0.2 AU.

EXAMPLE 4 pH and Temperature Optima

Clostridium coskatii (PS02) grew optimally at an initial pH between 5.8 and 6.5; growth occurred at initial pH values between 4.0 and 8.0 (FIG. 13 a). When cultured in unbuffered media with an initial pH of 6.0, a final pH of 4.5 was measured. Cell growth was significantly inhibited by undissociated acetic acid when the concentration exceeded 50 mM. Clostridium coskatii showed better growth characteristics between pH 4.5 and 5.5 when compared to Clostridium autoethanogenum (FIG. 4); this trait might be particularly useful for an industrial process.

In addition to the collection of cell density measurements at various pH points, final fermentation products (acetate and ethanol) were also measured for batch fermentations using buffered fermentation media in a pH range from 4.0 to 8.5. Optimal pH conditions for production of acetate were at a pH of 5.85, at which a volumetric concentration of 11.0 g/L of acetate was produced in 120 hours. The optimum of ethanol production was in a pH range from 6.0 to 6.5, at which a volumetric concentration of 9.9 g/L of ethanol was produced in 120 hours (FIG. 5).

The optimal temperature for growth of Clostridium coskatii was 37° C. and the temperature range in which Clostridium coskatii (PS02) grew was 26-43° C. (FIG. 6).

Fermentation broth was analyzed for ammonia, ortho-phosphate, sodium, potassium, lactate, and osmolality using a Nova Bioprofile 300A biochemistry analyzer (Waltham, Mass.). Organic acid and alcohol analysis was conducted using an Agilent 1200 liquid chromatograph equipped with a Hi-Plex H analytical HPLC column (300×7.7 mm; PL1170-6830; Polymer Labs, Palo Alto, Calif.) equilibrated in aqueous 5 mM H₂SO₄ at a flow rate of 1 mL/min. Identification and confirmation of organic acids and alcohols in the broth fraction were performed on an Agilent 6890N gas chromatograph (GC) equipped with a 5975B electron-impact mass spectrometer (MS) and DB FFAP capillary column (15 m×250 μm×0.25 μm film, #122-3212, Agilent Technologies, Santa Clara, Calif.). Gas chromatography conditions were: Inlet=230° C.; oven programming=35-180° C. at 37°/min., MS interface=240° C., helium flow=1.7 mL/min.

EXAMPLE 5 Fatty Acid Methyl Ester Analysis

The fatty acid methyl ester composition of cellular biomass was determined for Clostridium coskatii (PS02), Clostidium ragsdalei, Clostridium autoethanogenum, and Clostridium ljungdahlii. Correlation coefficients for pair-wise comparisons showed that Clostridium coskatii (PS02) diverged in a range from 5% to 7% from other ethanologenic clostridia based on the cell membrane lipid composition. Divergence was driven by the concentration of 5 lipid components: 1,1-dimethoxy-hexadecane; 2-hexyl-cyclopropaneoctanoic acid, methyl ester; (Z)-13-Octadecenal; 1,1-dimethoxy-dodecane; and methyl tetradecanoate. Independent measurements of C. autoethanogenum are reported to demonstrate method reproducibility. (FIGS. 7 a, 7 b, and 7 c)

Fatty acid methyl ester analysis was performed on an Agilent 6890N GC equipped with a 5975B electron-impact mass spectrometer (MS) and Ultra 2 capillary column according to the MIDI method of Shutter and Dick (2000). Peak identity was confirmed with a bacterial fatty acid methyl ester standard (47080U, Supelco, Bellefonte, Pa.).

EXAMPLE 6 16S rRNA Sequences

Phylogenetic analysis of the 16S rDNA gene sequence (SEQ ID NO 3; FIG. 8 a) of Clostridium coskatii (PS02) indicated that the organism belonged within clostridial rDNA homology group 1 (Collins et. al., 1994; Johnson & Francis 1975). There was a high overall level of conservation in the 16S rDNA sequences for representatives of the ethanologenic clostridia cluster. Pairwise analyses of 16S rRNA sequences for representatives of the ethanologenic clostridia cluster exceeded 99.27% similarity for all comparisons. In this cluster, Clostridium coskatii (PS02) was located within a group of five other clostridia; C. ljungdahlii C-01 (Gen Bank Accession No. GU139550), C. ljungdahii ERI-2 (GU129551), C. ragsdalei (AY170378), C. ljungdahlii PETC (GU139552) and C. autoethanogenum (Y18178) (FIG. 8 b). Based on this analysis, Clostridium coskatii (PS02) is closely related to other ethanologenic acetogens in clostridial rDNA homology group 1, and is most closely related (99.86%) to C. ljungdahlii ERI-2 based on the Neighbor-Joining/UPGMA method (FIG. 9).

The primary structure of the 16S rDNA gene is highly conserved, and species having 70% or greater genomic DNA similarity usually have more than 97% sequence identity for the 16S rDNA gene (Stackebrandt and Goebel, 1994). As with other organisms, these differences were not randomly scattered through the 16S rDNA sequence, but were concentrated in certain hypervariable regions. These hypervariable regions are known to be taxon specific and can only be determined by sequence analysis. Two regions of entropy in the 16S rDNA alignments provided identifying sequence features for each of the six ethanologenic acetogens. Clostridium coskatii (PS02) could be uniquely identified by the presence of key differentiating DNA bases within the hypervariable region of the 16S rDNA sequence (See Table H and FIG. 10). These unique sequence attributes are an identifying feature of this organism. Table H. 16S rDNA base positions that distinguish Clostridium coskatii (PS02) from other ethanologenic acetogens.

Starting  Base SEQ ID NO. Position Sequence SEQ ID 215 GARACTGRTTT NO. 1 SEQ ID 1525 AACGAAAGAGGACGCGCCCGAA NO. 2

The 16S rRNA analysis of the six clostridial ethanologens presented in this work shows that these bacteria are closely related on a phylogenetic level, and are well above the 97% sequence identity threshold requirement for determining individual species. The utility of 16S rRNA gene sequence for establishing new species for organisms that differ by <97% is well established. Scores of >97% are not clear, and require the use of methods with higher resolution such as DNA-DNA reassociation, or DNA fingerprinting (Janda and Abbot, 2007; Konstantinos and Tiedje, 2005).

Genomic DNA was isolated from ethanologenic clostridia using the ChargeSwitch® gDNA Mini Bacterial Kit using directions supplied by the manufacturer (#CS11301, Invitrogen, Carlsbad, Calif.). The full 16s rDNA sequence was performed according to the procedures described by Chandler et al. (1997). The universal primers used corresponded to positions 0005F and 1513R for the 1500 base pair (bp) sequence. Cycle sequencing of the 16S amplification products was carried out using DNA polymerase and dye terminator chemistry. The samples were electrophoresed on an ABI 3100 AVANT Genetic Analyzer. Sequence alignments and analyses were completed using BioEdit software version 7.0 (Hall, 1999). For reported sequences, G, A, T, C represent Guanine, Adenine, Thiamine, and Cytosine, respectively. The codes used for ambiguous bases is as follows: R (A or G),Y (C or T),W (A or T),S (C or G),K (G or T). The reproducibility of sequencing results was confirmed by comparing three independent sequencing runs for each organism. Three 16S rDNA sequences were deposited with GenBank since they resolved sequencing gaps associated with previously deposited sequences, or in the case of C. ljungdahlii C-01, the sequence did not previously exist in GenBank. These sequences were deposited under the following acquisition numbers: C. ljungdahlii C-01 (Gen Bank Accession No. GU139550), C. ljungdahii ERI-2 (GU129551), and C. ljungdahlii PETC (GU139552).

EXAMPLE 7 PCR-Based DNA Fingerprinting

One method for comparing closely related organisms is DNA fingerprinting by REP-PCR. This method makes use of DNA primers complementary to naturally-occurring, highly conserved repetitive DNA sequences that are present in multiple copies in most bacteria. The length and concentration of the amplicons that result from PCR provides a highly specific DNA fingerprint that can differentiate closely related species, or may be used to establish organisms that are genetically identical.

Three REP-PCR methods were used for DNA fingerprinting of ethanologenic acetogens, which included repetitive extragenic palindromic elements (REP-PCR), conserved repetitive DNA elements (BOX-PCR) and entrobacterial repetitive PCR intergenic consensus sequences (ERIC-PCR).

For BOX-PCR, the PCR products from the six ethanologenic clostridia were generated and compared (FIG. 11). All organisms had bands of approximately 1122, 587, and 323 bp in common. Clostridium coskatii (PS02) was missing bands of approximately 868, 714, 362 and 301 bp. Statistical analysis by Pearson UPGMA correlation of PCR amplicons showed that Clostridium coskatii (PS02) was most closely related to Clostridium autoethanogenum (76.1%), and Clostridium ljungdahlii PETC (75.7%; FIG. 12). The magnitude of differences between amplicons that were generated by BOX-PCR appeared to be least informative due to the low number of amplicons generated, and the similarity in their masses. This result suggests that there are a low number of target BOX palindromic elements present in these genomes, and these elements are more highly conserved than those generated by REP-PCR and ERIC-PCR. Regardless, all ethanologenic clostridia were still readily shown by BOX-PCR to be different, and varied in a range between 24% and 90.1% similar.

The REP-PCR products from the six ethanologenic clostridia were generated and compared (FIG. 13). Seven major PCR amplicons were generated from Clostridium coskatii (PS02) using the REP-PCR method: They were 1884, 1436, 1139, 860, 785, 284, and 185 bp. The 284 bp amplicon was common with all ethanologenic clostridia, but varied in intensity among the six organisms. Additionally, the amplicon at 185 bp in Clostridium coskatii (PS02) was also present in Clostridium ljungdahlii PETC and ERI-2, but at a much lower intensity. The remaining PCR products for Clostridium coskatii (PS02) were unique to this organism. Statistical analysis by Pearson UPGMA correlation of PCR amplicons showed that Clostridium coskatii (PS02) was most closely related to Clostridium ragsdalei at 40.9% similarity. The range for REP-PCR similarity scores varied between 2.6% and 40.9% similar (FIG. 14). The REP-PCR method provided the greatest level of differentiation between Clostridium coskatii (PS02) and other ethanologenic clostridia, and would be the preferred DNA fingerprinting method for future bacterial typing studies.

The ERIC-PCR products from the six ethanologenic clostridia were generated and compared (FIG. 15). More than seventeen major PCR amplicons were generated from Clostridium coskatii (PS02) using the REP-PCR method. Under optimized conditions, the ERIC-PCR method provided a higher background of PCR products, apparently due to the lack of probe specificity. Nevertheless, statistical analysis of the amplicon patterns by Pearson UPGMA correlation showed that Clostridium coskatii (PS02) was most closely related to Clostridium ljungdahlii PETC at 73.5% similarity (FIG. 16). The range for REP-PCR similarity scores (42.7 to 73.5%) was much narrower than other methods, and indicated that REP-PCR may be less desirable than the REP-PCR method for bacterial typing of ethanologenic acetogens.

Genomic DNA was isolated from ethanologenic clostridia using the ChargeSwitch® gDNA Mini Bacterial Kit using directions supplied by the manufacturer (#CS11301, Invitrogen, Carlsbad, Calif.). Three REP-PCR methods were used to generate amplicons from genomic DNA: These were (a) repetitive DNA elements (BOX-PCR), repetitive extragenic palindromic elements (REP-PCR), and enterobacterial repetitive intergenic consensus sequences (ERIC-PCR). REP-PCR for the three methods was carried out as described by Rahmati et al., (2005) with modifications proposed by MacCannel et al., (2006). Primers were synthesized by Invitrogen Corporation using the sequences provided by Rahmati et al., (2005). Molecular typing and statistical analysis of amplicon patterns was completed using BioNumerics 4.01 software (Applied Maths, Ft. Worth, Tex.). Two molecular weight markers were loaded on the gels at a concentration of approximately 0.1 to 0.3 μg (100 bp DNA ladder, 10488-058, Invitrogen; and pUC19/Sau3A 1 digest, AM7760, Invitrogen); however, molecular weight assignments were based on the AM7760 standard.

EXAMPLE 8 Comparison of G+C Content of DNA

The mol % G+C of the DNA from Clostridium coskatii (PS02) was 32.5%±0.5% G+C (n=5), which was 3 to 10% higher than other known ethanologenic clostridia. The G+C content of these bacteria fall within the expect range of low G+C gram positive bacteria (Drake, et al., 2002; and Drake et al., 2006). G+C content for Clostridium coskatii (PS02) and the three most closely related ethanologenic clostridia (according to DNA fingerprinting) is provided in Table I.

TABLE I G + C content for clostridial species Species G + C Content Clostridium autoethanogenum DSMZ 10061 25.9 ± 0.6% G + C Clostridium ljungdahlii PETC DSMZ 13528 22.5 ± 0.5% G + C Clostridium ragsdalei ATCC BAA-622 29.5 ± 0.5% G + C Clostridium coskatii PS02 32.5 ± 0.5% G + C

Bacterial cells were disrupted with french pressure cell and the DNA was purified on hydroxyapatite according to the procedure of Cashion et al. (1977). Next, the DNA was hydrolyzed with P1 nuclease and the nucleotides were dephosphorylized with bovine alkaline phosphatase (Mesbah et al. 1989). The resulting deoxyribonucleosides were analyzed by HPLC. The HPLC System (Shimadzu Corp., Japan) consisted of the following modules: LC-20AD solvent delivery module, DGU-3A online degasser, CTO-10AC column oven, SIL-20A automatic sample injector, and a SPD-6A UV spectrophotometric detector. Chromatograms were analyzed by using the CLARITY (Version 2.4.1.93) software package (DataApex Ltd., Czech Republic). The analytical column was a VYDAC 201SP54, C₁₈, 5 μm (250×4.6 mm) equipped with a guard column 201GD54H (Vydac, Hesperia, Calif. 92345, USA). The liquid chromatography conditions were: Temperature 45° C., 10 μl sample, solvent 0.3 M (NH₄)H₂PO₄/acetonitrile, 40:1 (v/v), pH 4.4, 1.3 ml/min (adapted from Tamaoka & Komagata, 1984). The reference DNA used for system calibration included: Non-methylated Lambda-DNA (Sigma), GC-content 49.858 mol % (Mesbah et al., 1989) and 3 DNAs for which complete genome sequences were published (http://ergo.integratedgenomics.com/GOLD/): Bacillus subtilis DSMZ 402 (43.518 mol % G+C); Xanthomonas campestris pv. campestris DSMZ 3586^(T) (65.069 mol % G+C); and Streptomyces violaceoruber DSMZ 40783 (72.119 mol % G+C). The G+C value was calculated from the ratio of deoxyguanosine (dG) and thymidine (dT) according to the method of Mesbah et al. (1989).

EXAMPLE 9 DNA-DNA Hybridization

DNA fingerprinting studies indicated that Clostridium coskatii (PS02) was most closely related to Clostridium autoethanogenum, Clostridium ljungdahlii PETC, and Clostridium ragsdalei. Based on these results, a DNA-DNA hybridization study was performed with these organisms to determine similarity of the genomic DNA. DNA-DNA hybridization is unequivocally the preferred method for proposed new species and for the definitive assignment of an organism with ambiguous properties to the correct taxonomic unit (Stackebrandt et al., 2002). The phylogenetic definition of a species includes that (a) the purified DNA molecules show 70% or greater DNA-DNA relatedness, (b) have a 5° C. or less ΔTm for the stability of heteroduplex molecules, and (c) the phenotypic characteristics should agree with this definition (Wayne et al, 1987; Stackebrandt and Goebel, 1994).

All pairings for Clostridium coskatii met species requirements when a threshold value of 70% DNA-DNA similarity was used (Table J.). This result indicated that Clostridium coskatii (PS02) represented a new bacterial species. All other pairings were below the 70% threshold value except for Clostridium ljungdahlii and Clostridium autoethanogenum, for which the confidence interval overlapped at the 70% threshold value.

TABLE J DNA-DNA hybridization results Clostridium Clostridium autoethanogenum ljungdahlii PETC PS02 DSMZ 1006 DSMZ 1352 Clostridium 66.5 ± 4.0 X X autoethanogenum DSMZ 10061 Clostridium 68.9 ± 1.0 76.7 ± 7.0 X ljungdahlii PETC DSMZ 13528 Clostridium ragsdalei 64.3 ± 4.1 58.7 ± 3.6 62.6 ± 6.1 ATCC BAA-622

Genomic DNA was sheared and released from bacterial cells using a French pressure cell (Thermo Spectronic) and was purified by chromatography on hydroxyapatite as described by Cashion et al. (1977). DNA-DNA hybridization was carried out as described by De Ley et al. (1970) under consideration of the modifications described by Huss et al. (1983) using a model Cary 100 Bio UV/VIS-spectrophotometer equipped with a Peltier-thermostatted 6×6 multicell changer and a temperature controller with in-situ temperature probe (Varian). Results are reported as the average from two independent analyses, which differed by less than 10%. Similarity values were reproducible in a range of approximately 10% of the reported value.

EXAMPLE 10 Ethanol and Acetate Productivity

Long-term (>1,000 hours) Continuous Stirred Tank Reactors (CSTR) experiments were performed to determine ethanol and acetate productivity of Clostridium coskatii (PS02) under steady-state fermentation conditions. A fermentation balance for this organism was determined while growing in CSTR mode on a simple inexpensive chemically-defined medium and using synthesis gas as the electron and carbon source. During steady-state conditions, the utilization of trace metals was measured to investigate nutrient deficiencies with the chemically-defined medium.

A Sartorious Biostat B CSTR was operated at 37° C. utilizing Acetogen C5 media, which was prepared using the strict anaerobic technique described by Balch and Wolfe (1976). This media was essentially the same as Acetogen C3 medium, except that sodium sulfide, yeast extract, and the MES buffer were omitted, and an antifoam agent, such as Antifoam A (Sigma Chemical, St. Louis, Mo.) was added to the medium at a final concentration of 20 mg/L. The pH of the fermentation was controlled throughout the duration of the process at 5.20±0.1 using 5M sodium hydroxide.

Semi-continuous (20 minute intervals) analysis of inlet and outlet gas concentrations of CO, H₂, CO₂, N₂, CH₄, and ethanol was performed using a ThermoElectron Prima δB process gas mass spectrometer. Reactor operation was divided into two major processes: Reactor startup, which was completed under batch conditions, and CSTR ethanol production phase. After inoculation of the reactor with a 10% inoculum, the reactor was operated in batch mode until the cell density increased to 0.2 g dry cell weight per liter of broth (g DCW/L). At that time, a continuous feed consisting of Acetogen C5 media was started using a dilution rate (D) of 0.2 day⁻¹. During start-up and throughout the ethanol production phase, a synthesis or waste gas consisting of CO, H₂ and CO₂ in a composition of 37% CO, 21.68% CO₂, 35.1% H₂ and 6.22% N₂ was continuously introduced into the bioreactor. Gas flow and agitation were raised at a rate to maintain hydrogen uptake in excess of 70%. Finally, the feed media rate was increased to a final value of D=0.5 day⁻¹ over a time period of 48 hours after the cell density exceeded 0.60 g DCW/L.

The maximum doubling time for pre-steady state chemostat cultures during early exponential growth phase for Clostridium coskatii (PS02) when using Acetogen C5 media was 0.064 hr⁻¹. During ethanol production phase, and steady-state chemostat growth, the growth rate decrease by 75 to 100-fold, and remained stable for up to 1,150 hours of CSTR operation (FIG. 17).

The elemental profile of biomass collected from a CSTR fermentation of C. coskatii (PS02) was compared to published results for C. ljungdahlii PETC (Tanner et al., 1993). When compared to C. ljungdahlii PETC, the sample of C. coskatii biomass contained significantly more phosphorus and sulfur, but a similar level of potassium and oxygen (FIG. 18). This result indicated that there were significant differences in the cellular composition of elements for these two types of ethanologenic clostridia.

Gas uptake, biomass production, and product formation by Clostridium coskatii (PS02) was measured for a CSTR over a period of 1,150 hours (FIGS. 19 and 20). During this period, Clostridium coskatii was grown on Acetogen C5 media with 0.1 g cysteine free base per liter, under 37% CO, 21.68% CO₂, 35.1% H₂ and 6.22% N₂. By approximately 200 hours, the gas flow, agitation, dilution rate, and cell density reached their final steady-state values of 0.27 vvm, 900 rpm, 0.5 day⁻¹, and 1.733 g DCW/L, respectively. After 10 days of CSTR operation, and a dilution rate of 0.5 day⁻¹, a steady-state condition was achieved for the reactor (at 440 hours). Both LC and GC-MS analyses of the broth showed two major products were produced from the fermentation; they were acetate, and ethanol (FIG. 21). There were also trace amounts of ethyl acetate and formic acid, ethyl ester, which were acid-catalyzed chemical reaction products of metabolic intermediates (formate) or final end products (acetate and ethanol) (FIG. 21).

After reaching a steady state condition, a mass balance was completed on the fermentation to confirm that Clostridium coskatii was using the Acetyl CoA pathway. The mean and standard deviation for the uptake of CO, and H₂, and the emission of CO₂ and ethanol vapor were calculated for a 470 hour time-period that started at 440 hours and ended at 910 hours. In addition to measuring gaseous compounds, the amount of biomass, ethanol, acetate, and the fermentation volume were measured in the broth fraction during this period (FIGS. 22 a and 22 b). The mean values for this mass balance were:

-   -   Ethanol production: 5.365 mmol/L/hr     -   Acetic acid production: 3.745 mmol/L/hr     -   Ethanol vented: 0.144 mmol/L/hr     -   Biomass production: 0.0533 mmol/L/hr     -   CO uptake: 28.27 mmol/L/hr     -   H₂ uptake: 20.58 mmol/L/hr     -   CO₂ uptake: −8.52 mmol/L/hr (negative uptake)

TABLE K Electron balance under steady-state CSTR conditions for Clostridium coskatii (PS02). Component Concentration, mmol Electron equivalents CO (in) 28.27 56.54 H₂ (in) 20.58 41.16 CO₂ 8.52 n/a Biomass 0.0533 n/a Ethanol (out) 5.509 66.11 Acetate (out) 3.745 29.96 Electrons in 97.700 Electrons out 96.068 Balance 1.017 Error, % 1.04%

The electron balance in Table K shows excellent agreement between the concentration of electron donors feeding into the process and the concentration of electron acceptors (acetate and ethanol) that are produced from the bacterium. Closure of the electron balance to 1.04% provides a confirmation that no other major products were present in the fermentation broth (Table K).

The carbon balance for clostridial ethanologens, such as Clostridium coskatii (PS02) is complicated by the fact that there are both consuming, and producing reactions for CO₂ when a mixture of CO and H₂ is co-metabolized (see reactions on p. 5). Oxidation of CO by the carbon monoxide dehydrogenase is the main reaction for producing CO₂ under minimal media conditions, and the acetyl Co-A pathway, with electrons derived through the oxidation of H₂ by the hydrogenase is the main consuming pathway for uptake of CO₂. For a biochemical system that is producing a mole ratio of roughly 1:1 ethanol to acetate, every mole of H₂ that is oxidized results in 0.41666 moles of CO₂ are fixed to acetyl CoA (this value is calculated from the average H₂ to CO₂ ratio for acetate [2:1] and ethanol [3:1] production). For the example below, the amount of CO₂ consumed through electrons acquired from the hydrogenase can be estimated by dividing the total mmoles of hydrogen utilized by 2.40.

The carbon balance for this CSTR fermentation is shown in Table L. The carbon balance shows that the metabolism of Clostridium coskatii (PS02) fits the acetogenic model. Furthermore, the measured error for the experiment is less than 1%, which again confirms that all reactants and products have been accurately measured, and that there are no other major products that are being produced in this syngas fermentation.

TABLE L Carbon balance under steady-state CSTR conditions for Clostridium coskatii (PS02). Non-carbon containing compounds (H₂) are included in the table for calculation of the fixed CO₂ value, but they are not directly used in the carbon balance. CO H₂ CO₂ → CO₂ Ethanol Acetate Biomass mmoles of reactants or products: 5.16 1.72 0.716 3.29 1.00 0.26 0.014 mmoles of carbon equivalents: 5.16 0.716 → 3.29 2.00 0.52 0.014 Total carbon equivalents: 5.876 →  5.824 Error, % 0.9%

EXAMPLE 11 Effect of an Organic Carbon Source on Ethanol and Acetate Productivity-Validation of a Chemically-Defined Minimal Medium

The effect of the organic carbon source, yeast extract was evaluated in long-term (>700 hours) Continuous Stirred Tank Reactors (CSTR) containing Clostridium coskatii under steady-state fermentation conditions. Through these studies, it was shown that Clostridium coskatii grew well in the absence of complex organic carbon sources. This trait had not been previously demonstrated for other known clostridial ethanologens, and therefore, was unique to Clostridium coskatii. CSTR studies were completed with a chemically-defined minimal medium, and a medium supplemented with 0.1 g/L yeast extract to further characterize the effect of complex organic carbon sources on ethanol and acetate production by Clostridium coskatii.

A Sartorious Biostat B CSTR was operated at 37° C. utilizing Acetogen C5 media, as previously described in Example 10. Reactor conditions and operating procedures were identical to those described previously in Example 10.

The effect of yeast extract on ethanol and acetate production by Clostridium coskatii (PS02) was measured for the two CSTRs over a period of 720 hours (FIG. 23). During reactor startup and before establishment of steady-state conditions, acetate and ethanol production was similar for the control reactor, which contained no yeast extract in the feed medium, and the reactor feed supplemented with 0.1 g/L yeast extract. Similarity in product trends during reactor startup was due to the carry over of nutrients from the inoculum; these carry over nutrients were depleted by more than 60% of their original concentration at 192 hours based on the dilution rate of 0.2 day⁻¹, and differences in the acetate and ethanol trends became significant at this time. When the dilution rate was increased to 0.5 day⁻¹ at 200 hours, the differences in acetate and ethanol production became more pronounced, in that the ethanol concentration increased to a steady-state condition of 24 g/L in the control reactor, but dropped to less than 1 g/L in the reactor supplemented with 0.1 g/L yeast extract. These changes in ethanol production were linked with a 2-fold increase (23 g/L) in acetate production for the reactor supplemented with 0.1 g/L yeast extract, while the acetate levels in the control reactor remained at a constant, steady-state level of approximately 12 g/L throughout the duration of the experiment. These data show that a chemically-defined minimal media, equivalent to Acetogen C5 media is optimal for production of biofuels via synthesis gas fermentation using Clostridium coskatii.

While the present invention has been described in terms of its preferred embodiments, those skilled in the art will recognize that the Clostridium coskatii bacterium of the invention can be utilized in a variety of ways within the spirit and scope of the appended claims. Accordingly, the present invention should not be limited to the specific embodiments described above. 

We claim:
 1. A method of producing ethanol comprising, combining a carbon source, an electron source and Clostridium coskatii ATCC No. PTA-10522 under conditions which allow the Clostridium coskatii to convert the carbon source to ethanol.
 2. The method of claim 1 wherein the carbon source is CO₂.
 3. The method of claim 1 wherein the carbon source is CO.
 4. The method of claim 1 wherein the carbon source is an organic carbon.
 5. The method of claim 1 wherein the electron source is H₂ or CO.
 6. The method of claim 1 wherein the carbon source and the electron source are provided by syngas.
 7. The method of claim 1 wherein combining of the carbon source, the electron source and Clostridium coskatii ATCC No. PTA-10522 is performed under anaerobic conditions.
 8. The method of claim 7 wherein the anaerobic conditions are established using the Balch technique.
 9. The method of claim 1 wherein the conditions further comprise adding a liquid medium that is chemically defined.
 10. The method of claim 9 wherein the liquid medium is Acetogen C3 medium.
 11. The method of claim 9 wherein the liquid medium is an aqueous nutrient medium.
 12. The method of claim 1 wherein the conditions include the use of fermentor containing the Clostridium Coskatii as immobilized cells.
 13. The method of claim 1 wherein the conditions include suspending the Clostridium Coskatii in an aqueous media.
 14. The method of claim 1 wherein the combining takes place in a continuous flow type reactor.
 15. The method of claim 14 wherein the combining takes place in a continuous stirred tank reactor. 